AU2009352613A1 - Device for disinfecting water by means of anodic oxidation - Google Patents

Device for disinfecting water by means of anodic oxidation Download PDF

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Publication number
AU2009352613A1
AU2009352613A1 AU2009352613A AU2009352613A AU2009352613A1 AU 2009352613 A1 AU2009352613 A1 AU 2009352613A1 AU 2009352613 A AU2009352613 A AU 2009352613A AU 2009352613 A AU2009352613 A AU 2009352613A AU 2009352613 A1 AU2009352613 A1 AU 2009352613A1
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Prior art keywords
water
storage tank
feed pipe
redox
control
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AU2009352613A
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AU2009352613B2 (en
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Martin Alexander Goldmaier
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AUTARCON GmbH
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AUTARCON GmbH
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/467Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
    • C02F1/4672Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electrooxydation
    • C02F1/4674Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electrooxydation with halogen or compound of halogens, e.g. chlorine, bromine
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/006Water distributors either inside a treatment tank or directing the water to several treatment tanks; Water treatment plants incorporating these distributors, with or without chemical or biological tanks
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • C02F1/4618Devices therefor; Their operating or servicing for producing "ionised" acidic or basic water
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/008Mobile apparatus and plants, e.g. mounted on a vehicle
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/009Apparatus with independent power supply, e.g. solar cells, windpower, fuel cells
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/46Apparatus for electrochemical processes
    • C02F2201/461Electrolysis apparatus
    • C02F2201/46105Details relating to the electrolytic devices
    • C02F2201/4612Controlling or monitoring
    • C02F2201/46125Electrical variables
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/46Apparatus for electrochemical processes
    • C02F2201/461Electrolysis apparatus
    • C02F2201/46105Details relating to the electrolytic devices
    • C02F2201/4612Controlling or monitoring
    • C02F2201/46125Electrical variables
    • C02F2201/46135Voltage
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/46Apparatus for electrochemical processes
    • C02F2201/461Electrolysis apparatus
    • C02F2201/46105Details relating to the electrolytic devices
    • C02F2201/4612Controlling or monitoring
    • C02F2201/46145Fluid flow
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/46Apparatus for electrochemical processes
    • C02F2201/461Electrolysis apparatus
    • C02F2201/46105Details relating to the electrolytic devices
    • C02F2201/4616Power supply
    • C02F2201/46165Special power supply, e.g. solar energy or batteries
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/46Apparatus for electrochemical processes
    • C02F2201/461Electrolysis apparatus
    • C02F2201/46105Details relating to the electrolytic devices
    • C02F2201/4616Power supply
    • C02F2201/4617DC only
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/003Downstream control, i.e. outlet monitoring, e.g. to check the treating agents, such as halogens or ozone, leaving the process
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/04Oxidation reduction potential [ORP]
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/05Conductivity or salinity
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/40Liquid flow rate
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/42Liquid level
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/20Controlling water pollution; Waste water treatment
    • Y02A20/208Off-grid powered water treatment
    • Y02A20/212Solar-powered wastewater sewage treatment, e.g. spray evaporation

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

The invention relates to a device for disinfecting water by means of anodic oxidation, wherein a reservoir (10) is provided for disinfected water, wherein a feed line (15) leads from the water to be disinfected into the reservoir (10), wherein a reactor (4) for the anodic reaction of the water is arranged in the feed line (15), wherein the reservoir (10) has a redox sensor (5) for measuring the redox potential, wherein the water feed from the feed line (15) into the reservoir (10) is intermittent.

Description

Autarcon GmbH C 3048 PCT/27.02.2012 5 Device for the purification on water by anodic oxidation Field of invention The invention relates to a device for the purification of water by anodic oxidation. 10 State of the art Anodic oxidation is performed by what is commonly known as electrolytic cell, which is em bodied as a set of plate electrodes. Such electrolytic cell is commercially available, for ex ample, from the company G.E.R.U.S. The production of free chlorine from NaCl dissolved in 15 water is performed by such anodic oxidation reactor in the form of an electrolytic cell, in the process of which hypochloric acid is formed which disinfects the water. So far, the technol ogy is known and does not need to be explained in more detail at this point. Furthermore, there is known what is referred to as a redox sensor. By means of a redox sen sor the redox potential is determined, which is a voltage, on the basis of which it is possible 20 to make statements on the Nater quality with respect to its bacterial contamination de pending on the amount of measured voltage. It is not possible, however, to make a direct statement on the chlorine content of the water depending on the measured voltage, as the voltage is also influenced by both the pH value and the temperature of the water. However, it is possible to make assumptions about when a certain voltage shows a good or a bad wa 25 ter quality on the basis of information found in tables. This means that the redox potential allows a statement on the disinfection potential of the water. Said redox potential is a very weak signal and thus prone to interference. As already explained elsewhere, the purification of water by anodic oxidation is already known. In this context a device for the purification of water comprising two water circuits is 30 known. In one of the water circuits, the chlorination of the water by anodic oxidation takes place, whereby in another water circuit, which is essentially separated from the first one, the chlorinated water is channelled into a storage tank. Consequently, the redox sensor is not connected to the reactor for anodic oxidation by any means. The amount of necessary pipe material for a device according to the state of the art is considerable. Devices for the 35 purification of water are needed particularly in developing countries, therefore it is always intended to manufacture such devices for the purification of water as cost-effectively as possible and, in addition, to embody them as robustly as possible. Due to the fact that the state of the art provides two water circuits, the device is, on the one hand, more prone to interference, and more expensive on the other.
C 3048 PCT The task underlying the present invention is, therefore, to provide a device for the purifica tion of water by anodic oxidation, which can be manufactured at a considerably lower cost and more simply than in the state of the art by embodying the device with one single water circuit only. This means that the device is intended to work with one single water circuit 5 only, which comprises both the reactor for the anodic reaction as well as the redox sensor. Description of the invention A device of the kind described above, which works with one single water circuit but which is still capable of providing purified drinking water in a sufficient quality and quantity, is char 10 acterized by the features according to Claim 1. In this process, a storage tank for purified water is provided having a feed pipe leading from the water to be purified into the storage tank, whereby a reactor for the anodic reaction of the water is arranged within the feed pipe. A redox sensor is arranged within the storage tank itself, which can be purchased, for example, from the company Jumo. By means of said redox sensor, the redox potential is 15 measured which is a value indicating the water quality. As already described elsewhere, the redox potential is a very weak signal and thus also prone to interference. As the redox sensor is electrically connected to the reactor both by means of the feed pipe and the water entering the storage tank, the voltage applied to the reactor falsifies the measuring signal of the redox sensor such that it is not suitable to func 20 tion as a value with respect to a statement on water quality. In so far, according to the in vention it is provided that the water supply from the feed pipe into the storage tank is em bodied in a discontinuous form so that no electric connection exists between the redox sen sor on the one hand, which is situated within the storage tank, and the reactor carrying out the anodic oxidation on the other, which means that no electric connection exists between 25 the control circuit and the load circuit. The control circuit comprises the sensors, in particu lar, the redox sensor; the load circuit comprises the oxidation reactor. In order to supply water in a, discontinuous manner into the storage tank, in particular, an arrangement is provided, which may, for example, be embodied as a tube, wherein the tube comprises a number of openings through which the water is discharged into the storage 30 tank in the form of a discontinuous water jet or in the form of drops. In this context it is also conceivable that the arrangement is embodied as a disk interrupting the water jet or as a finger which rotates below the water jet at a respective velocity. According to another feature of the invention, the device comprises a control, wherein the voltage applied to the reactor is controlled by said control depending on the magnitude of 35 the redox potential. More precisely, said control is connected to a pump within the feed pipe. This means that the voltage applied to the reactor is controlled in relation to the amount of water which is supplied through the pump, depending on the measured redox potential, the conductance of the water, and the bacterial contamination. At least one level sensor is arranged within the storage tank in order to prevent the storage tank from flowing 40 over or a particular amount of water to be stored from falling below a certain value. In addition, the feed pipe comprises a flow meter which is also connected to the control. The figures below describe the invention in more detail.
C 3048 PCT Fig. 1 shows an illustration of the device for the purification of water; Fig. la shows the ar rangement for the generation of a discontinuous water jet; Fig. lb schematically shows a rotating finger for interruption of the water jet; Fig. 2 shows the control. 5 The invention relates to a device for the purification of water, whereby such device shall particularly be applied in developing countries. It may be used there as transportable equipment for the purification of drinking water. The device is provided with a power sup ply, preferably, a photovoltaic generator (1), which supplies both the pump (3) and the an odic oxidation reactor (4) with electric current by means of a control (2). A DC/DC converter 10 (6) is arranged between the anodic oxidation reactor and the control. The redox sensor (5) is connected to the control (2) by means of a measuring line (7). The two level sensors (11) and (12) arranged within the storage tank (10) are connected to the control by further measuring lines (13), wherein the control is connected to the pump by a line (14). The feed pipe marked (15), within which also the flow meter (16) is arranged, constitutes 15 the connection between the pump (3), the anodic oxidation reactor (4), the flow meter (16) and the storage tank (10). As already explained, the redox sensor (5) is arranged within the storage tank (10), measuring the redox potential as a voltage there. The measured value itself, i.e. the redox potential, is very weak so that interferences directly lead to a falsifica tion of the measured value such that said value is not suitable any more for providing a 20 statement with respect to the water quality. In this context it is provided that the feed pipe (15) comprises an arrangement (20) for discontinuous water supply at its end above the storage tank (10). Such device for discontinuous water supply may be embodied according to Fig. la as a tube section or as a cylinder, comprising a number of openings (21) in order to allow the discharge of thewater into the storage tank (10) in the form of droplets or, at 25 least, in a discontinuous form'. According to Fig. 1b, a rotating finger (25) below a water out let is provided, which continuously interrupts the jet of water. If a continuous jet of water were able to enter storage tank (10) from the feed pipe (15), an electric connection be tween the redox sensor within the storage tank and the anodic oxidation reactor would ex ist through the water jet. This would mean that interferences caused within the oxidation 30 reactor by the voltage and the electric current would be transferred by the water to the redox sensor within the storage tank. By means of unbundling the water jet into partial jets, or by a continuous short-term interruption of the jet, which means a discontinuous supply of water into the storage tank, there is no direct connection between the redox sensor, on the one hand, and the oxidation reactor on the other. Any interferences at the redox sensor 35 can therefore be completely eliminated, which, in particular, does not necessitate any addi tional cost with respect to a possible use of particular circuits which are intended to prevent such interferences. The control shown in Fig. 2 acts as follows: If the solar radiation directed at the photovoltaic generator is large enough, and if there is 40 sufficient water for purification purposes available, and if the storage tank (10) is not full, the control will switch on both the DC/DC converter (6) and the pump. Depending on the water flow, a current target value (Isoii) is indicated by the anodic oxidation reactor. There by the control generates a respective PWM signal, as a consequence of which a voltage gen erated by the DC/DC converter is applied to the plates of the anodic oxidation reactor and a C 3048 PCT current depending on the conductance of the water list appears. Due to the current within the anodic oxidation reactor, free chlorine is formed, which reacts with the substances pre sent in the water (bacteria, dust, etc.) and which is measured by means of the redox poten tial. Said current is compared to the specified redox target value and amplifies or reduces 5 the specified current target value (I set). By means of a current sensor the current (I actual) is constantly compared to the current target value (I set) and adapted, if necessary. The control interprets the effect of the bacteria on the system as interference. No direct measured data exist on its influence; however, its value is reflected in the redox potential. If the number of bacteria colonies is large, a larger amount of oxidizing substances is required, or, respec 10 tively, used, which results in a reduction of the redox voltage. An effective entry of bacteria can be assumed with a time constant of several hours. Therefore, the redox potential is the true control variable of the system. I4

Claims (8)

1. Device for the purification of water, comprising a storage tank (10) for retention of 5 the purified water; whereby a feed pipe (15), leads from the water to be purified to the storage tank (10); whereby a reactor (4) for anodic reaction of the water is ar ranged within the feed pipe (15), whereby the storage tank (10) comprises a redox sensor (5) for measuring the redox potential, and whereby water supply from the feed pipe (15) into the storage tank (10) is performed discontinuously. 10
2. Device according to Claim 1, characterized in that the feed pipe (15) comprises an arrangement (20) for discontinuous water supply into the storage tank (10) at the discharge for the purpose of discontinuous water supply into the storage tank (10).
3. Device according to Claim 2, characterized in that the arrangement (20) is embodied as a tube comprising a multitude of openings (21). 15
4. Device according to Claim 2, characterized in that the arrangement (20) is embodied as a finger (25) interrupting the water jet.
5. Device according to one of the preceding claims, characterized in that the device comprises a control (2), wherein by means of control (2) the voltage applied to the reactor (4) depending on the magnitude of the redox potential, the conductivity, the 20 applied water flow and the degree of bacterial contamination is controlled.
6. Device according to one of the preceding claims, characterized in that the control is connected to a pump (3) that is arranged within the feed pipe (15).
7. Device according to one of the preceding claims, characterized in that the control is connected to at least one level sensor (11, 12) within the storage tank (10). 25
8. Device according to one of the preceding claims, characterized in that the feed pipe (15) comprises a flow meter (16), which is connected to the control. IS C3048 PCT Summary The invention refers to a device for the purification of water, comprising a storage tank (10) 5 for retention of the purified water; whereby a feed pipe (15), leads from the water to be purified to the storage tank (10); whereby a reactor (4) for anodic reaction of the water is arranged within the feed pipe '(15), whereby the storage tank (10) comprises a redox sensor (5) for measuring the redox potential, and whereby water supply from the feed pipe (15) into the storage tank (10) is performed discontinuously. 10 (Fig.1) 15 I2
AU2009352613A 2009-09-18 2009-09-18 Device for disinfecting water by means of anodic oxidation Ceased AU2009352613B2 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/DE2009/001313 WO2011032527A1 (en) 2009-09-18 2009-09-18 Device for disinfecting water by means of anodic oxidation

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AU2009352613A1 true AU2009352613A1 (en) 2012-04-12
AU2009352613B2 AU2009352613B2 (en) 2015-09-17

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US (1) US9701550B2 (en)
EP (1) EP2477951B1 (en)
CN (1) CN102630217B (en)
AU (1) AU2009352613B2 (en)
BR (1) BR112012005959B1 (en)
CA (1) CA2774111C (en)
DE (1) DE112009005258A5 (en)
WO (1) WO2011032527A1 (en)
ZA (1) ZA201201897B (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019200472A1 (en) * 2018-04-17 2019-10-24 Emersa Engineering Inc. Fluid treatment apparatus and methods
EP4249441A1 (en) * 2022-03-20 2023-09-27 Donato Patrissi In pipe drinking water generator with minimal infrastructure dependence

Family Cites Families (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2935124A1 (en) * 1979-08-30 1981-03-12 Reis, August K., Prof. Dr.med., 8000 München METHOD FOR DISinfecting WATER.
US4724059A (en) * 1986-07-11 1988-02-09 Purichlor Technology Ltd. Automated chlorine generator
US4767511A (en) * 1987-03-18 1988-08-30 Aragon Pedro J Chlorination and pH control system
US5422014A (en) * 1993-03-18 1995-06-06 Allen; Ross R. Automatic chemical monitor and control system
US5756051A (en) * 1993-05-12 1998-05-26 Overton; James Michael Apparatus and method for an anodic oxidation biocidal treatment
DE29709241U1 (en) * 1997-05-27 1997-08-28 Preisendanz Hans Dr Med Self-sufficient house water disinfection system
DE60036582T2 (en) * 1999-08-06 2008-06-26 Puricore International Ltd. Electrochemical treatment of an aqueous solution
JP2002088493A (en) * 2000-09-14 2002-03-27 Honda Motor Co Ltd Water electrolysis system
US20020070107A1 (en) * 2000-12-07 2002-06-13 Usinowicz Paul J. Water purification system and process for treating potable water for at source use
JP4020787B2 (en) * 2001-04-27 2007-12-12 三洋電機株式会社 Water treatment equipment
JP3957476B2 (en) * 2001-05-28 2007-08-15 三洋電機株式会社 Water treatment equipment
US6780306B2 (en) * 2002-02-12 2004-08-24 Bioelectromagnetics, Inc. Electroionic water disinfection apparatus
EP1807216B1 (en) * 2004-11-03 2014-12-24 Nelson Irrigation Corporation Water deflection assembly
US7402252B2 (en) * 2005-06-20 2008-07-22 Ecolab Inc. Automated electrolyte addition for salt water pools, spas, and water features
KR100841664B1 (en) * 2006-05-30 2008-06-26 전치중 Electro-Chemical Water Processing Apparatus and Method of the same
US20090242419A1 (en) * 2008-03-28 2009-10-01 Aldridge John W On-site on-demand chlorine gas generator
US20120152760A1 (en) * 2009-06-24 2012-06-21 Aquatech Water Purification Systems Pty Ltd Water treatment method and system

Also Published As

Publication number Publication date
AU2009352613B2 (en) 2015-09-17
DE112009005258A5 (en) 2012-08-09
US20120175271A1 (en) 2012-07-12
CA2774111A1 (en) 2011-03-24
BR112012005959B1 (en) 2019-04-30
BR112012005959A2 (en) 2016-03-15
US9701550B2 (en) 2017-07-11
CN102630217A (en) 2012-08-08
EP2477951A1 (en) 2012-07-25
CN102630217B (en) 2014-12-10
ZA201201897B (en) 2012-11-28
WO2011032527A1 (en) 2011-03-24
EP2477951B1 (en) 2019-01-23
CA2774111C (en) 2018-03-20

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